PODBIELNIAK, INC. - Industrial & Engineering Chemistry (ACS

The state of glass recycling in the US. Americans dispose of some 10 million metric tons of glass annually. Most of it ends up in the trash.... SCIENC...
1 downloads 0 Views 2MB Size
wmte&if&iB/fâMigfaand th ΑΚΟΙ/ΑΦ π/ε woxLD/ AQUAZONS HYDRA-JETS

PODBIELNIAK CONTACTORS a n d SOLVENT EXTRACTORS are a v a i l ­ a b l e in a v a r i e t y of m o d e l s d e s i g n e d f o r y o u r specific process, r a n g i n g i n c a p a c i t y f r o m a c o m p l e t e l a b o r a t o r y e x t r a c t i o n p l a n t o f 5 0 0 cc p e r m i n u t e t o i n t e r m e d i a t e a n d c o m m e r c i a l size u n i t s u p ίο» 9 0 , 0 0 0 G A L L O N S PER H O U R . '"**' *·

PODBIELNIAK H Y D R A Z O N S A N D D U O Z O N S PROCESSING S O Y B E A N O I L I N A VEQEJLJkBLE * * * O I L R E F I N I N G PLANT

W i l l Penicillin Change

the

Petroleum Skyline?

BATTERY O F PODBIELNIAK P E T R O Z O N S IJM* A M O D E R N PETROLEUM REFINERY

PODBIELNIAK ψ Ι Α Ν Ι Ζ Ο Ν — EXPERIMENTAL • ' W O R K O N URANIUM REFINING

for

exciting

news

LIFT

A N D

FOLD

OUT

TURN YOUR LOSSES INTO GOLD! ! MODERNIZE YOUR P L A N T OPERATIO W R I T E FOR Q U E S T I O N N A I R E .

eets using PODBIELNIAK Contactors AFTER

FLOWSHEET "A" illustrate c o m p l i c a t e d assemblage of equi BEFORE using P O D B I E L N I A K TACTORS.

AFTER

It d r a m a t i c a l l y d e m o n s t r a t e s t h e p l e x i t y of a batch p r o c e s s r e q u i r e d lube treating plant with convent type centrifuges.

FLOWSHEET "Β" PODBIELNIAK CONTACTOR S T R A T C O REACTOR P L A N T

/""LOW £>/AG/?AM ?OVr//VtX?U5 LUBC TRSAT/Νσ

PLANT

T h e " c h a n g i n g s c e n e " in p l a n t pro ing using P O D B I E L N I A K CON T O R S is w e l l d e m o n s t r a t e d in t h e f l o w s h e e t s s h o w n at left on page. TWENTY-FOUR centrif are replaced w i t h FOUR d e s k PODBIELNIAK CONTACTOR

Z9.J3BI

IT SOLVENT EXTRACTION WITH SOLVENT

mizon utomatic operaraction and soliry. investment and ost. îneration allows inventory.

RECOVERY

AFTER

IH^H

LEGEND 1. L i q u i d - l i q u i d c o u n t e r c u r r e n t extraction and separation. II. Flash evaporation of solvent. III. Solvent stripping column. IV. Solvent vapor recovery system.

IEPHENOLIZING PROCESS FOR AQUEOUS WASTES

bielniak C h e m i z o n 5. E x i t s t r e a m s c e n trifugally clarified. 6. Six extraction stages in one C h e m i z o n .

7. C a u s t i c t r e a t e r r e generates solvent. 8. F l o w r a t e s o f 1000 G .Ρ.Μ . combined streams.

Economic Comparison of Podbielniak Centrifugal S o l v e n t Extractors V s . Mi Centrifuge Apparatus for Three-step Continuous Extraction of Penicillin BEFORE Process Flow Sheet Complicated because of large number of separate units of equipment required to obtain equivalent of three-state extraction.

AFTER Process Flow Sheet Simplified since more than 5 stages extraction available in a single, comp unit requiring only one set of pumps stead of three.

Refrigeration Refrigeration of broth required in first step. Cleaning Necessary to disassemble centrifuges for cleaning requiring at least one hour per unit. Maintenance Large number of operating parts and complicated flow sheet requires constant attention of large maintenance force.

Refrigeration Refrigeration of broth in first step required. Cleaning Extractors cleaned in 10-15 minutes w out disassembly by simple flus operation. Maintenance Extractors "down t i m e " for maintena is less than 0.02% of "operating t i m

P O D B I E L N I A K , 341

EAST

OHIO

ST.

·

CHICAGO

INC. 1 1 , ILL.

The ΰ//Μβ/Λ/β

SCE/l/Ε in modern plant processing fit WMJJM:» AFTER BEFORE

PODBIELNIAK PODBIELNIAK

A d v a n t a g e s of P o d b i e l n i a k 1. R a f f i n a t e a n d e x t r a c t streams centrifugally clari­ f i e d — r e d u c i n g load on strippers. 2. High capacity throughput w i t h low h o l d u p p e r m i t s rapid attainment of equilib­ rium in one hour—special advantage to "blocked out" operations.

EXTRACTION

OF CATALYTIC CYCLE

Petrozon

3. " O f f T e s t " Material r e d u c e d to a m i n i m u m . 4. H i g h p r e s s u r e a n d t e m p e r ­ a t u r e c o n d i t i o n s w i t h fully automatic operation. 5. L o w c a p i t a l i n v e s t m e n t a n d maintenance costs.

CONTINUOUS URANIUM

A d v a n t a g e s specific to catalytic stock and aromatic extractions 1. P r o c e s s a l l o w s 50% i n c r e a s e of v i r g i n catalytic c r a c k e r c h a r g e . 2. C o k e - b u r n i n g r e q u i r e m e n t s r e ­ d u c e d by 5 0 % . 3. P r o d u c t i o n of P o l y g a s o l i n e i n ­ crease. 4. O c t a n e level of t o t a l g a s o l i n e i m ­ proved. 5. L o w s o l v e n t i n v e n t o r y m a k e s ex­ pensive selective solvent systems feasible.

ACID LEACH LIQUOR

A d v a n t a g e s of P o d b with Solvent 1. S o l v e n t e x t r a c t i o n p l a n t in a packaged unit. 2. A d a p t a b l e t o a l l l i q u i d liquid extraction systems. 3. P o d b i e l n i a k C h e m i z o n w i l l separate systems with spe­ c i f i c gravity d i f f e r e n t i a l a s l o w as 0.015.

το URANIUM RECOVERY

CHEMIZON

SALT SOLUTION EXTRACT SURGE

COUI

EXTRACTION

SOLVENT RECOVERY

URANIZON WASTE

CONTINUOUS

STOCK

Advan 1. P h e n o l c o n c e n t r a t i o n r e d u c e d to 5-10 P.P.M. 2. E x c e l l e n t c a u s t i c economy.

3. C l o s systi 4. Immc gene vent

cf/ANô/νβ seE/i/ε

From eye-dropper capacity (200 c c / min) to a Niagara Cascade —90,000 GPH

PODBIELNIAK MIDGET CONTACTOR (200 cc/min)

PROCESS INDUSTRIES U S I N G PODBIELNIAK C O N T A C T O R S A N D SOLVENT EXTRACTORS AQUAZONS Crude O i l Desalting · Contaminated Oils I n s u l a t i n g Oils · Lube O i l Purification Antibiotics

·

BIOZONS Biochemicals Penicillin

Medicinal*

CHEM1ZONS Beverages · Chemicals C o a l Tar Derivatives · Coke O v e n Chemicals G e r m i c i d e s a n d Insecticides · P e t r o c h e m i c a l s Plastics DUOZONS A n i m a l O i l s · Fish O i l s Vegetable Oil Degumming

PODBIELNIAK C O N T I N U O U S SOAP PROCESSING PLANT

HYDRA-JETS Hormones Antibiotics · Chemicals · Petrochemicals · V e g e t a b l e Oils HYDRAZONS A n i m a l O i l s · Fish O i l s Lacquers a n d D r y i n g Oils Resin W a s h i n g * V e g e t a b l e O i l s MINERALZONS Rare E a r t h R e f i n i n g PETROZONS Lube O i l Refining · Petrochemicals Extraction Petroleum Refining PHASEZONS Phase S e p a r a t i o n a n d C l a r i f i c a t i o n i n A l l Industries * Beverages P u l p a n d P a p e r · Yeast S e p a r a t i o n SOAPRAZONS C o n t i n u o u s S o a p Processing Synthetic Detergents URANIZONS U r a n i u m Recovery

PODBIELNIAK C H E M I Z O N S FOR R E M O V I N G PHENOL FROM COKE O V E N WASTE LIQUORS

PODBIELNIAK INSTALLATION I N A PETROCHEMICAL PLANT

PODBIELNIAK, INC.

VEGEZONS ^ A n i m a l O i l s R e f i n i n g · Fish O i l s Vegetable Oils Refining

3 4 1 E. O H I O ST. · C H I C A G O W r i t e in f o r Engineering Questionnaire Brochure N o . 1 0 , a n d Technical Bulletin N o . C-1 1 0 . N o o b l i g a t i o n f o r our investigation o f your current operations.

see

Refining

11, ILL.

reverse side f o r " C H A N G I N G S C E N E " in m o d e r n p l a n t orocessinq flowsheets using P O D B I E L N I A K CONTACTORS